US2101534A - Urea-formaldehyde condensation products - Google Patents

Urea-formaldehyde condensation products Download PDF

Info

Publication number
US2101534A
US2101534A US34300A US3430035A US2101534A US 2101534 A US2101534 A US 2101534A US 34300 A US34300 A US 34300A US 3430035 A US3430035 A US 3430035A US 2101534 A US2101534 A US 2101534A
Authority
US
United States
Prior art keywords
urea
formaldehyde
condensation products
formaldehyde condensation
aqueous
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US34300A
Inventor
Edgar Donald Edwards
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US34300A priority Critical patent/US2101534A/en
Application granted granted Critical
Publication of US2101534A publication Critical patent/US2101534A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G12/00Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
    • C08G12/02Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes
    • C08G12/04Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds
    • C08G12/10Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds with acyclic compounds having the moiety X=C(—N<)2 in which X is O, S or —N
    • C08G12/12Ureas; Thioureas

Definitions

  • the bulk of the aqueous material is usually repreferably not below 15 C.,by any suitable means 10 moved by filtration and the white crystalline and allowed tostand for at least 48 hours or 10 preoipitateis then dried usually at ordinary room until complete precipitation of the reaction prodtemperatures or at elevated temperatures under uct has taken place. Precipitation usually begins 3 controlled conditions. yThe drying of the crystalafter about '12 hours standing. When theprecipiline mass offers .difliculties in that the crystals tation is complete the crystalline material is recakeyin hard lumps which delays the drying time moved by filtration.
  • the crystalline mass is then 15 considerably, thus making the operation ineftreated with ethyl; alcohol to form a slurry and flcientl This caking of the crystals is probably. again filtered to remove the alcohol; This operadue to the cementing action of the'dissolved portion is preferably carried out two times.
  • the material may be dried 20- the filtering operation.
  • the material thus proby any convenient means either at room temperaduced inhard lumps and cakes presents difiiculture or at a slightly elevated temperature.
  • the ties for further use, requiring grinding and crystalline mass thus prepared dries completely screening or sieving, The material thus prepared and thoroughly and results in a fluffy material is often not thoroughly dry and must here-dried substantially free from any lumps and caking.
  • urea is dis: of an improved procedure for preparing'the resolved inwater and the para-formaldehyde added action product of urea and formaldehyde.
  • ther object is the provisionoi an improved pro- In place of the ethyl alcohol which is used to 30 cedure for preparing dimethylol urea in a physlwash the crystalline mass after filtration, methyl,
  • breaking the resulting may be, mentioned the aromatic hydrocarbons cake into Small pieces, treating Wi h a iq i such as benzol, toluol and xylol, and aliphatic miscible with Water but a non-solvent f0! the hydrocarbons as petroleum ether, gasoline, naph. 45
  • convenient modification for the washing of the Exampz 1 crystalline mass may comprise centrifuging in a 50 Grams basket type centrifuge and after the bulk of the v aqueous material is removed spraying with the i liquid to remove the remaining aqueous material p I i as may adhere to the crystalline mass.
  • v solution is added variations in this respect will be readily apparent 55 to those skilled in the art.
  • the hydrogen ion concentration given in the example above is noted as 1.6, this may conveniently range between 6 and 9, yielding equally satisfactory results and without departing from the spirit of the invention
  • the material produced according to the procedure of the invention may be advantageously adapted for use as a moldingmaterial, as such, ccording to methods well known in the art. Further, the material may be adapted for use as a film-forming composition for particular purposes either alone or in combination withv other.
  • This invention presents as a principal advantage a method for producing the reaction product of urea and formaldehyde, which can be more readily and efliciently dried after the removal of the aqueous liquid by filtration and which does not substantially cake or harden into lumps on drying.
  • the reaction product of urea and formaldehyde produced in accordance with the present invention is more stable than material produced by present procedures, i. 6. dried directly after filtration.
  • the product made by myimproved method is also in a much more suitable physical condition for further use where it may be desired to dissolve it or react with other materials withthe urea and formaldehyde in aqueous solution thereby obtaining in caked form a crystalline precipitate of said reaction product in aqueous liquor which is a non-solvent for the precipitated reaction product, separating substantially all said aqueous liquor from the crystalline caked precipitate, breaking the resulting cake into small pieces, then forming a slurry of said precipitate with a water miscible liquid which is selected from the class consisting of acetone and alcohols and which is a non-solvent'for said precipitate, separating said precipitate from the non-solvent. and completely drying the precipitate thereby obtaining said urea-formaldehyde reaction product in a fiufi'y form substantially free from lumps and caked particles.

Description

a w- 1 1 1 i 2,101,534.
UREA-FORMALDEHYDE CONDENSATIQN i PBODUCTSIQ M DonaldEdwards Edgar, Phlladelphlarrau. assign- Y M or.to ,l l.fl. v du Pont deNemours & Company,
i .wilmingtonfiDel 'a corporation .of Delaware No Drawing. Application-August i, 1935, i 1 'SerialNo. 34,300 i c c A L l (01.260 3) I Thiswinvention relates io condensation prodsodium acid phosphate (NaHzPO il 511 buffer;
ucts of -urea and :formaldehyde, andi more -'par- The hydrogen ion concentration of the solution ticularly toan improved procedure for preparis then adjustedto a pH value of 7.6 by the addiing dimethylol urea in a physicalcondition more "tion of sodium hydroxide solution "using Phenol satisfactory for further use. l n Redas an indicator and comparing; with standard 5 The'reaction product of urea" and 5 aqueous color tubes. The ur'ea is thenflissdlved'in the formaldehyde ordinarily precipitates as a white formaldehyde solution thus prepaiedfThe liquid erystalline solidwhich.isreadily'soluble in water. is keptrat a temperatureof b'elo'w 25 1C., and i c The bulk of the aqueous material is usually repreferably not below 15 C.,by any suitable means 10 moved by filtration and the white crystalline and allowed tostand for at least 48 hours or 10 preoipitateis then dried usually at ordinary room until complete precipitation of the reaction prodtemperatures or at elevated temperatures under uct has taken place. Precipitation usually begins 3 controlled conditions. yThe drying of the crystalafter about '12 hours standing. When theprecipiline mass offers .difliculties in that the crystals tation is complete the crystalline material is recakeyin hard lumps which delays the drying time moved by filtration. The crystalline mass is then 15 considerably, thus making the operation ineftreated with ethyl; alcohol to form a slurry and flcientl This caking of the crystals is probably. again filtered to remove the alcohol; This operadue to the cementing action of the'dissolved portion is preferably carried out two times. After tion of the crystals from which the aqueous mathe last treatment and removal of as much alcohol terial has not been completely removed during as possible by filtration the material may be dried 20- the filtering operation. The material thus proby any convenient means either at room temperaduced inhard lumps and cakes presents difiiculture or at a slightly elevated temperature. The ties for further use, requiring grinding and crystalline mass thus prepared dries completely screening or sieving, The material thus prepared and thoroughly and results in a fluffy material is often not thoroughly dry and must here-dried substantially free from any lumps and caking.
. after grinding and screening. Instead of.aqueous formaldehyde I may use h e tio h s a O j the provision Dara-formaldehyde. In this case the urea is dis: of an improved procedure for preparing'the resolved inwater and the para-formaldehyde added action product of urea and formaldehyde. A furas a solid. i
ther object is the provisionoi an improved pro- In place of the ethyl alcohol which is used to 30 cedure for preparing dimethylol urea in a physlwash the crystalline mass after filtration, methyl,,
cal condition inwhich it will be more satisfactory propyl, butyl or other similar aliphaticalcohols '0 fu th imm d 8-. A further ject is as well as such materialsas acetone, ethyl ether the provision of. an improved method for the prepof ethylene glycol, methyl ether of ethylene glycol aration of .dimethylol urea which will obviate the and similar materials may housed, the principal 5 ss y of th us f d asti rindin procedures requirement being that the liquid is miscible with i to place the material in condition for further use, water,
and which will produce a material'of uniform- If desired the crystalline mass, after the al- .quality and relatively uniform physical condition. oohol treatment, may be treated with a liquid 40 Otherobjects will appear hereinafter. l which is miscible with the alcohol used and which 40 The o j ar mpli h d. y rem vin does not react with the product of the reaction as much water from the crystalline precipitate as f rea, and formaldehyde. Among such liquids practical y fil ra ion, breaking the resulting may be, mentioned the aromatic hydrocarbons cake into Small pieces, treating Wi h a iq i such as benzol, toluol and xylol, and aliphatic miscible with Water but a non-solvent f0! the hydrocarbons as petroleum ether, gasoline, naph. 45
urea-formaldehyde reaction products, filtering thas and the like. and drying. i The washing with alcohol may be repeated any The following example isillustrative of a pre number of times as may be found practical; A
ferred embodiment of the invention: convenient modification for the washing of the Exampz 1 crystalline mass may comprise centrifuging in a 50 Grams basket type centrifuge and after the bulk of the v aqueous material is removed spraying with the i liquid to remove the remaining aqueous material p I i as may adhere to the crystalline mass. Many To theaqueous formaldehyde,v solutionis added variations in this respect will be readily apparent 55 to those skilled in the art. While the hydrogen ion concentration given in the example above is noted as 1.6, this may conveniently range between 6 and 9, yielding equally satisfactory results and without departing from the spirit of the invention The material produced according to the procedure of the invention may be advantageously adapted for use as a moldingmaterial, as such, ccording to methods well known in the art. Further, the material may be adapted for use as a film-forming composition for particular purposes either alone or in combination withv other.
synthetic resins and/or suitable softening agents.
This invention presents as a principal advantage a method for producing the reaction product of urea and formaldehyde, which can be more readily and efliciently dried after the removal of the aqueous liquid by filtration and which does not substantially cake or harden into lumps on drying. The reaction product of urea and formaldehyde produced in accordance with the present invention is more stable than material produced by present procedures, i. 6. dried directly after filtration. The product made by myimproved method, as compared to the urea-formaldehyde reaction product as conventionally made, is also in a much more suitable physical condition for further use where it may be desired to dissolve it or react with other materials withthe urea and formaldehyde in aqueous solution thereby obtaining in caked form a crystalline precipitate of said reaction product in aqueous liquor which is a non-solvent for the precipitated reaction product, separating substantially all said aqueous liquor from the crystalline caked precipitate, breaking the resulting cake into small pieces, then forming a slurry of said precipitate with a water miscible liquid which is selected from the class consisting of acetone and alcohols and which is a non-solvent'for said precipitate, separating said precipitate from the non-solvent. and completely drying the precipitate thereby obtaining said urea-formaldehyde reaction product in a fiufi'y form substantially free from lumps and caked particles.
DONALD EDWARDS EDGAR.
US34300A 1935-08-01 1935-08-01 Urea-formaldehyde condensation products Expired - Lifetime US2101534A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US34300A US2101534A (en) 1935-08-01 1935-08-01 Urea-formaldehyde condensation products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US34300A US2101534A (en) 1935-08-01 1935-08-01 Urea-formaldehyde condensation products

Publications (1)

Publication Number Publication Date
US2101534A true US2101534A (en) 1937-12-07

Family

ID=21875541

Family Applications (1)

Application Number Title Priority Date Filing Date
US34300A Expired - Lifetime US2101534A (en) 1935-08-01 1935-08-01 Urea-formaldehyde condensation products

Country Status (1)

Country Link
US (1) US2101534A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442897A (en) * 1944-08-21 1948-06-08 Us Of Ameria As Represented By Process for resinifying ligno-cellulosic materials with urea-formaldehyde
US2541139A (en) * 1947-07-18 1951-02-13 American Cyanamid Co Process for blending alkyd resin and ether of dimethylol urea
US2634246A (en) * 1950-11-13 1953-04-07 Allied Chem & Dye Corp Resin for wet strength paper and process for making it

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442897A (en) * 1944-08-21 1948-06-08 Us Of Ameria As Represented By Process for resinifying ligno-cellulosic materials with urea-formaldehyde
US2541139A (en) * 1947-07-18 1951-02-13 American Cyanamid Co Process for blending alkyd resin and ether of dimethylol urea
US2634246A (en) * 1950-11-13 1953-04-07 Allied Chem & Dye Corp Resin for wet strength paper and process for making it

Similar Documents

Publication Publication Date Title
US2282026A (en) Treatment of polyvinyl acetal resins
US2101534A (en) Urea-formaldehyde condensation products
US2319649A (en) Method of making purified sirup
US1812693A (en) Manufacture of new derivatives from sulphite cellulose waste
US1723800A (en) Utilization of sulphite cellulose waste liquor
US2377961A (en) Manufacture of water-soluble egg albumen
US2397307A (en) Decolorizing protein
US2326369A (en) Preparation and use of sugar refining adsorbent
US2238714A (en) Purification of alkyl ethers of cellulose
US2132434A (en) Process of preparing a protein material
US2464167A (en) Process for the recovery of pentaerythritol
US1938512A (en) Process for the manufacture of salts of organic acids from albuminoids and the like
US1947717A (en) Cocoa product and process of making same
US2094359A (en) Preparation of base-exchanging synthetic resin
US2019415A (en) Aluminium formate and process of making the same
US2651662A (en) Treatment of pentaerythritol mother liquor
US2716613A (en) Water soluble adhesive and a process of making it
US1683702A (en) Process for purifying phenol formaldehyde resins
US868445A (en) Process of preparing casein soluble to a neutral solution.
US1175439A (en) Recovery of potash from calcined alunite.
DE820440C (en) Process for the preparation of aminocarboxylic acids by hydrolysis of their lactams
US2340672A (en) Oleoresin treatment
US2643953A (en) Process of making adhesive from lignocellulose
US2386289A (en) Treatment of pentaerythritol
US2851433A (en) Treatment of residual liquor